US4462911A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Detoxification or decontamination of effluents and/or flue gases
Assignee: Andritz Ruthner Industrieanlagen AG
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Filing: 1982-04-16
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Granted: 1984-07-31
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Expires: 2002-04-16
Abstract
Abstract This invention provides a process for detoxifying or decontaminating liquid effluents and/or waste gas containing poisonous chromium (VI) NOx by reacting these with each other with formation of chromium (III) and higher oxide(s) of N. Optionally in addition another suitable reducing agent may be used. The process is particularly useful, for example, in a plant such as a stainless steel pickling plant where both these chemical components are available. Preferably liquid-liquid extraction may be used to extract and recover nitric acid formed as an oxidation product and preferably if additional chromium (VI) is required, this may be provided by electrolytic oxidation of chromium (III) to chromium (VI) in a suitable chemical circuit.
Inventors
- 👤 Friedrich Samhaber
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 22:40
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/54; B01D53/56; C; C02; C02F; C02F2101/00; C02F2101/10; C02F2101/20; C02F2101/22; C02F2103/00; C02F2103/18; Y; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/911; Y10S210/912; Y10S210/913; Y10S210/918; Y10S210/919
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
48 words
A process for detoxifying or decontaminating an effluent containing chromium (VI), and waste gas containing NO x , wherein said effluent and said waste gas are reacted together, thereby causing chromium (VI) to react with NO x , with formation of chromium (III) and higher oxide(s) of N.
Claim 2
Dependent Claim
48 words
A process for detoxifying or decontaminating an effluent containing chromium (VI), and waste gas containing NO x , wherein said effluent and said waste gas are reacted together, thereby causing chromium (VI) to react with NO x , with formation of chromium (III) and higher oxide(s) of N.
Claim 3
Dependent Claim
28 words
A process as claimed in claim 1, wherein NO x -containing waste gas is contacted with water or acidic washing water prior to reaction with chromium (VI) effluent.
Claim 4
Dependent Claim
29 words
A process as claimed in claim 1, wherein nitric acid, formed as an oxidation product of NO x , is removed from the reaction solution by extraction and recovered.
Claim 5
Dependent Claim
41 words
A process as claimed in claim 1, wherein for complete oxidation of NO x , chromium (VI) is provided by electrolytic oxidation of chromium (III) produced as a reaction product in the conversion of NO x to higher oxide(s) of N.
Claim 6
Dependent Claim
37 words
A process as claimed in claim 1, wherein the reaction solution is pumped along a circuit including being passed through a liquid-liquid extraction apparatus and a throughflow electrolytic cell and thereafter is recycled into a reaction chamber.
Claim 7
Dependent Claim
19 words
A process as claimed in claim 5, wherein the reaction chamber is provided in a waste gas washing installation.
Claim 8
Dependent Claim
119 words
A process for detoxifying or decontaminating effluent containing chromium (VI), and waste gas containing NO x , for example in a stainless steel pickling plant, wherein the waste gas is contacted with water or acidic washing water to dissolve NO x therein in a counter current waste gas washing installation and the chromium (VI) solution is reacted with the NO x in solution in the washing installation, whereafter the reaction solution is passed through a liquid-liquid extraction apparatus to extract nitric acid for recovery and thereafter the solution is passed to a through-flow electrolytic cell to oxidise chromium (III) to chromium (VI) which is recycled to the waste gas washing installation for subsequent reaction with NO x in solution.
Claim 9
Dependent Claim
119 words
A process for detoxifying or decontaminating effluent containing chromium (VI), and waste gas containing NO x , for example in a stainless steel pickling plant, wherein the waste gas is contacted with water or acidic washing water to dissolve NO x therein in a counter current waste gas washing installation and the chromium (VI) solution is reacted with the NO x in solution in the washing installation, whereafter the reaction solution is passed through a liquid-liquid extraction apparatus to extract nitric acid for recovery and thereafter the solution is passed to a through-flow electrolytic cell to oxidise chromium (III) to chromium (VI) which is recycled to the waste gas washing installation for subsequent reaction with NO x in solution.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-07-31 | 1988-01-30 | 1988-07-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-07-31 | 1992-01-30 | 1992-07-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-07-31 | 1996-01-30 | 1996-07-31 | $7700.00 | Window Closed / Lapsed |